U.S. patent number 3,862,072 [Application Number 05/408,988] was granted by the patent office on 1975-01-21 for thermosetting aqueous coatings containing branched hydroxy functional polyester and hydroxy functional polyether or polyester adducts of an at least trifunctional alcohol.
This patent grant is currently assigned to DeSoto, Inc.. Invention is credited to Kazys Sekmakas.
United States Patent |
3,862,072 |
Sekmakas |
January 21, 1975 |
**Please see images for:
( Certificate of Correction ) ** |
THERMOSETTING AQUEOUS COATINGS CONTAINING BRANCHED HYDROXY
FUNCTIONAL POLYESTER AND HYDROXY FUNCTIONAL POLYETHER OR POLYESTER
ADDUCTS OF AN AT LEAST TRIFUNCTIONAL ALCOHOL
Abstract
Thermosetting aqueous coatings are provided containing hydroxy
functional polyesters based on tricarboxylic acids, such as
trimellitic anhydride, reacted with excess diol to an acid number
in the range of 45-60, formaldehyde condensates, and from 5-40%,
based on total resin solids, of a polyether or polyester adduct of
an at least trifunctional alcohol having a molecular weight of at
least about 300. The polyether or polyester adduct lowers viscosity
at high solids content while minimizing the need for volatile
cosolvents, and it participates in the cure to increase the
flexibility and impact resistance of the cured coating.
Inventors: |
Sekmakas; Kazys (Chicago,
IL) |
Assignee: |
DeSoto, Inc. (Des Plaines,
IL)
|
Family
ID: |
26975535 |
Appl.
No.: |
05/408,988 |
Filed: |
October 23, 1973 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
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307099 |
Nov 16, 1972 |
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Current U.S.
Class: |
524/539; 427/375;
525/443; 525/508; 525/519; 525/442; 525/507; 525/509 |
Current CPC
Class: |
C09D
167/00 (20130101); C09D 167/00 (20130101); C08L
2666/14 (20130101); C09D 167/00 (20130101); C08L
2666/02 (20130101) |
Current International
Class: |
C09D
167/00 (20060101); C08g 037/34 (); C08g
051/24 () |
Field of
Search: |
;260/29.2E,29.2EP,29.4R,29.4UA,29.6NR,29.6TA,75R,842,850,860 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Goldstein; Melvin
Assistant Examiner: Danison; W. C.
Attorney, Agent or Firm: Dressler, Goldsmith, Clement &
Gordon, Ltd.
Parent Case Text
The present application is a continuation-in-part of my prior
application Ser. No. 307,099, filed Nov. 16, 1972.
Claims
I claim:
1. Thermosetting aqueous coating composition having a total solids
content of at least about 55% and comprising an aqueous medium
containing at least 80 parts of water for every 20 parts of
water-miscible volatile organic solvent and having dispersed
therein:
1. essentially oil-free, non-gelled hydroxy functional acidic
polyester formed by polyesterifying a polycarboxylic acid
component, of which tricarboxylic acid or anhydride thereof
selected from trimellitic of alpha-(2-carboxyethyl)-glutaric
provides at least 70% of the acidic functionality, the balance
being saturated dicarboxylic acid or anhydride, with a
stoichiometric excess of a polyalcohol component consisting
essentially of aliphatic diol, said polyalcohol component providing
from 1.1 up to about 2 hydroxy equivalents per equivalent of
carboxy in said polycarboxylic acid component, said polyester
having an acid number in the range of from about 45 to about 60 and
being dispersed in the aqueous medium with the aid of a base;
2. from 5% - 40%, based on total resin solids, of heat-hardening
formaldehyde condensate dispersible in the aqueous medium and
selected from aminoplasts and phenol-formaldehyde condensates;
and
3. polyether or polyester adduct of ethylene oxide, 1,2-propylene
oxide, or a lactone containing 3-14 carbon atoms with aliphatic
polyhydric alcohol containing at least three hydroxyl groups, said
adduct having a molecular weight in the range of from about 300 up
to about 5000, said adduct being present in the aqueous medium in
an amount of from 5% - 40%, based on total resin solids.
2. A coating composition as recited in claim 1 in which said
tricarboxylic acid component is a monoanhydride used in an amount
to provide at least 80% of the acidic functionality.
3. A coating composition as recited in claim 1 in which said
tricarboxylic acid component is trimellitic anhydride.
4. A coating composition as recited in claim 1 in which said diol
is a glycol.
5. A coating composition as recited in claim 3 in which said diol
is 2,2-dimethyl-3-hydroxypropyl-2,2-dimethyl-3-hydroxy propionate
and said formaldehyde condensate is an aminoplast resin.
6. A coating composition as recited in claim 1 in which said
polycarboxylic acid component includes a minor proportion of
saturated dicarboxylic acid.
7. A coating composition as recited in claim 1 in which the ratio
of hydroxy equivalents to carboxy equivalents is in the range of
1.2:1 to 1.6:1.
8. A coating composition as recited in claim 1 in which said
tricarboxylic acid is trimellitic anhydride and the ratio of
hydroxy equivalents to carboxyl equivalents is in the range of
1.25:1 to 1.4:1.
9. A coating composition as recited in claim 1 in which the total
solids content of said coating composition is at least about 60%,
and there are at least 90 parts of water for every 10 parts of
volatile organic solvent.
10. A coating composition as recited in claim 9 in which said base
is a volatile nitrogenous base and the coating composition has a pH
in the range of 6-11.
11. A coating composition as recited in claim 1 in which said
heat-hardening formaldehyde condensate is an aminoplast resin
present in an amount of from 10% - 30%, and said polyether adduct
has a molecular weight less than about 3,000.
12. A coating composition as recited in claim 1 in which said
polyether adduct is an adduct of 1,2-propylene oxide with an
aliphatic polyhydric alcohol containing 3 or 4 hydroxyl groups.
13. A coating composition as recited in claim 1 in which said
polyester adduct is an adduct of caprolactone with an aliphatic
polyhydric alcohol containing 3 or 4 hydroxyl groups.
14. A coating composition as recited in claim 1 in which said
adduct has a molecular weight in the range of about 400 to about
3,000.
15. Thermosetting aqueous coating composition having a total solids
content of at least about 55% and comprising an aqueous medium
containing at least 80 parts of water for every 20 parts of
water-miscible volative organic solvent and having dispersed
therein;
1. essentially oil-free, non-gelled, hydroxy functional acidic
polyester formed by polyesterifying trimellitic anhydride with
2,2-dimethyl-3-hydroxypropyl-2,2-dimethyl-3-hydroxy propionate in
stoichiometric excess, these components being the essential
components of the polyester, and being used in proportions
providing from 1.1 up to about 2 hydroxy equivalents per equivalent
of carboxy in said polyester, said polyester having an acid number
in the range of from about 45 to about 60 and being dispersed in
the aqueous medium with the aid of a base;
2. from 5% - 40%, based on total resin solids, of heat-hardening
aminoplast resin; and
3. polyether or polyester adduct of ethylene oxide, 1,2-propylene
oxide, or a lactone containing 3-14 carbon atoms with aliphatic
polyhydric alcohol containing three or four hydroxy groups, said
adduct having a molecular weight in the range of from about 300 up
to about 5,000, said adduct being present in the aqueous medium in
an amount of from 5% - 40%, based on total resin solids.
16. A coating composition as recited in claim 15 in which the ratio
of hydroxy equivalents to carboxy equivalents is in the range of
1.2;1 to 1.6:1 and said adduct is a polyether adduct of
1,2-propylene oxide with an aliphatic polyhydric alcohol containing
3 or 4 hydroxy groups.
Description
The present invention relates to thermosetting aqueous coatings
which have been modified to possess increased solids content at
lower solution viscosity while minimizing the presence of volatile
cosolvent and improving the flexibility and impact resistance of
the cured coatings.
In this invention a highly branched hydroxy functional acidic
polyester is formed by using a tricarboxylic acid (preferably in
the form of a monoanhydride) to provide at least 70% of the acidic
functionality and by using diols to supply an excess of hydroxy
functionality with polyesterification being continued until the
acid number is in the range of 45-60. This polyester is dispersed
in water with the aid of a base and a volatile water miscible
organic solvent and a water soluble or dispersible formaldehyde
condensate is incorporated in the aqueous medium together with
certain high molecular weight polyether or polyester adducts having
at least 3 hydroxy groups in an amount of from 5-40%, based on
total resin solids. It has been found that the presence of the high
molecular weight polyether adducts in the defined thermosetting
aqueous coatings significantly changes the characteristics of the
system to reduce the viscosity and the proportion of volatile
solvent which is needed. Further, by participating in the curing
reaction through hydroxy functionality, the polyether or polyester
adducts add significant flexibility and impact resistance to the
cured coatings. Also, the coatings exhibit improved flow properties
on baking, overcoming cratering and like surface nonuniformities so
that extraneous flow control agents can be omitted and foaming
tendencies are also reduced.
The polyesters which are used in this invention are essentially
free of oil or oil fatty acid, highly branched, and hydroxy
functional. As is well known, a polyester can be formed by the
polyesterification reaction of polycarboxylic acids with
polyalcohols. In this invention, the polyalcohol consists
essentially of diol and the polycarboxylic acids are essentially
tricarboxylic. Thus, these oil free polyesters do not resemble
alkyd resins which are oil-modified systems including a proportion
of polyol containing more than two hydroxyl groups, such as
glycerin.
Referring first to the polycarboxylic acids, at least about 70% of
the total carboxyl functionality must be supplied by a
tricarboxylic acid component, preferably employed in the form of a
monoanhydride. Trimellitic acid can be used, but trimellitic
anhydride is preferred. Another tricarboxylic acid monoanhydride
which can be used is alpha-(2-carboxyethyl)-glutaric anhydride.
Preferably, at least about 80% of the total carboxyl functionality
is supplied by the tricarboxylic acid component. The high
proportion of trifunctional acid produces extensive branching in a
water-dispersible structure of adequate molecular weight.
With such extensive branching accruing from the acid component, it
is necessary that the polyalcohol component consist essentially of
diol in order to avoid premature gelation of the polyester. Oil or
oil fatty acid are essentially absent since these are inconsistent
with the high performance film characteristics and the extensive
water dispersibility which are desired herein to form the
concentrated aqueous coatings which are intended to possess a total
solids content of at least 55%, preferably at least 60% by weight,
while still being of low solution viscosity permitting easy coating
of thin films.
The diol is preferably a glycol, e.g., the hydroxy groups are
carried by terminal carbon atoms in the aliphatic carbon chain. The
"neo" structure which denotes the presence of a tertiary carbon
atom is especially preferred to provide coatings of outstanding
characteristics. Thus, while any diol such as ethylene glycol,
propylene glycol, butylene glycol, diethylene glycol, or the like
may be used, a "neo" structure as is present in the commercial
ester diol 204 is particularly preferred. This diol has the
formula: ##SPC1##
The acid component may include a minor proportion of saturated
dicarboxylic acids, the term "saturated" here including aromatic
unsaturation as in phthalic acid or anhydride, iso- or
tere-phthalic acids. Adipic or succinic acids will illustrate the
aliphatic diacids.
Monofunctional reactants are largely excluded since these are lower
molecular weight.
The components which are subjected to polyesterification in one or
more stages must include an excess of hydroxy functionality. On an
equivalent basis, there should be at least 1.1 up to about 2
hydroxy equivalents per equivalent of carboxy. A ratio of from
1.2:1 to 1.6:1 being preferred, with best results at a ratio of
1.25:1 to 1.4:1.
The polyesterification reaction is itself entirely conventional,
except from the standpoint that the final acid number must be less
than about 60. Since the copolyester will gel at an acid number of
about 45, it will be apparent that the copolyesters of interest
herein must possess a narrow range of acidity of from about 45 to
about 60. At higher acidity, the resinification of the polyester is
inadequate to provide the rapid curing and outstanding film
characteristics which are desired.
The hydroxy functional polyester so-provided can be dispersed at
high solids content in aqueous medium with the aid of a base and a
volatile organic solvent, such as methyl ethyl ketone, 2-ethoxy
ethanol, 2-butoxy ethanol, dioxane, or other similar water-miscible
organic solvent. These volatilize during the bake and are,
therefore, objectionable. It is presently desired to minimize the
volatile solvent content of the coating by having at least 80 parts
of water for every 20 parts of volatile solvent and by making the
coating composition as concentrated as possible. This is quite
difficult in the absence of this invention.
The base used to form a salt with the unconsumed carboxyl
functionality in the polyester can be any base, but volatile
nitrogenous bases such as ammonia or an amine, such as triethyl
amine, are preferred. These are well known and entirely
conventional. Neutralization of the resin may be partial or
complete and the final aqueous composition may have a pH in the
range of 6-11, preferably 7.5-10.5. Again, this is a conventional
factor based on the use of bases to disperse acidic resins in
water.
The aqueous composition containing the dispersed polyester has
incorporated therein from 5-40%, preferably 10-30%, based on the
total weight of resin, of a heat-hardening formaldehyde condensate,
which can be dispersed in the aqueous medium. These constitute a
well known class primarily constituted by aminoplasts such as
urea-formaldehyde, hexamethoxy methyl melamine, and water
dispersible transethers thereof with ethanol or other lower
alcohol, benzoguanamine-formaldehyde and the like, including acidic
derivatives where the carboxyl group assists solubilization in
aqueous alkaline medium. Water soluble or dispersible
phenol-formaldehyde condensates are also useful, such as "A" stage
resols. These formaldehyde condensates can be used alone or in any
desired mixture.
From the standpoint of the final aqueous solution, the total solids
content should be at least about 55%, preferably at least about
60%. These total solids will include the polyester, the
formaldehyde condensate, the polyether or polyester adducts
described hereinafter, and any desired pigmentation.
The polyether adducts used in this invention are adducts of
ethylene oxide or 1,2-propylene oxide with an aliphatic polyhydric
alcohol containing at least three hydroxyl groups such as glycerin,
sorbitol or the like. Preferably, the alcohol groups are present in
the form of a plurality of methylol groups as in the compounds
trimethylol propane and pentaerythritol which are particularly
preferred. Propylene oxide is the preferred oxide.
The polyether adducts thus contain a plurality of hydroxy groups
and are water dispersible compounds having a molecular weight of at
least about 300, preferably at least about 400 up to about 5,000,
preferably less than about 3,000. A full thermosetting cure
generally requires a baking temperature of about 300.degree.F., and
the polyether adduct must be poorly volatile at such temperature in
order to remain in the film to control flow and participate in the
cure. At the same time, these hydroxy functional polyethers
function as a cosolvent in the aqueous composition, lowering
viscosity at high solids content and reducing the amount of
volatile solvent which is needed to maintain the ratio of volatile
solvent low, e.g., less than about 20 parts of solvent per 80 parts
of water, preferably less than about 10 parts of solvent per 90
parts of water.
The baking temperature will range depending on the time available.
At an oven temperature of about 350.degree.F., 30 minutes is quite
satisfactory. At lower temperatures of about 300.degree.F. up to
about 2 hours may be needed. At temperatures of about
550.degree.-625.degree.F., only 10-45 seconds are needed.
Importantly, the polyether adducts participate in the cure, become
a permanent part of the cured coatings, and significantly benefit
the flexibility and impact resistance which is obtained. With
tetrafunctional polyols such as pentaerythritol, film hardness is
also benefitted.
In addition to the polyether adducts described above, polyester
adducts of the same molecular weight range can also be used, these
being provided by the adduction of a lactone, such as
epsilon-caprolactone, with the same aliphatic polyhydric alcohols
containing at least 3 carbon atoms noted hereinbefore. It is found
that the polyester adducts produce thermosetting coatings which
possess superior color and color retention and which also provide
better corrosion resistance and better resistance to water.
The lactone-based polyesters are in commerce and are usually based
on epsilon-caprolactone which has the formula: ##SPC2##
These lactones are reacted with polyhydric alcohols in known
fashion to form adducts having the formula:
R ( O -- C -- CH.sub.2 -- CH.sub.2 -- CH.sub.2 -- CH.sub.2 --
CH.sub.2 -- OH) .sub.n
where R is the residue of an aliphatic polyhydric alcohol,
preferably glycerin, pentaerythritol, trimethylol propane, or the
like, and n is at least 3, preferably 3 or 4.
Other lactones which may be used are illustrated by butyrolactone,
gamma-valerolactone, beta-propiolactone, and the like. Thus, and
while epsilon-caprolactone is preferred, C.sub.3 - C.sub.14
lactones generally are useful.
The invention is illustrated in the examples which follow, in which
all parts are by weight, unless otherwise specified.
EXAMPLE 1
Parts by Weight
1.
1,200 Diethylene Glycol
950 Trimellitic Anhydride
230 Phthalic Anhydride
2 Dibutyl Tin Oxide Catalyst
50 Xylol (reflux solvent)
Set trap with xylol. Heat to 210.degree.C. and collect water. When
acid value of 95 is reached, decrease temperature to 180.degree.C.
Hold for acid value of 53-56 at 180.degree.-190.degree.C. Total
water collected, 180 grams. Remove trap, blow off xylol.
2. 733 Tetrol - molecular weight 405 (see Note 1)
3. 733 Hexamethoxy methyl melamine
4. 733 2-Ethoxy Ethanol
5. 2933 Deionized Water
6. 160 Dimethyl Ethanol Amine.
Add reactive solvent 2. Cool to 80.degree.C. and add water soluble
melamine 3, and solvent 4, water 5, and amine 6.
Final Characteristics
Solids: 49.1%
Gardner Viscosity: J-K
Color (Gardner Holdt) 1
Ratio of Resin Solids: ______________________________________ Water
Soluble Polyester: 60% Reactive Polyol: 20% Hexamethoxy Methyl
Malamine: 20% Ratio of Volatile Solvents: Deionized Water: 80%
2-Ethoxy Ethanol: 20% ______________________________________ Note 1
Polyoxypropylene derivative of pentaerythritol. Molecular weight:
405; Basic Functionality: 4; Hydroxy Number: 555, Viscosity: 2200
centipoises at 25.degree.C.
EXAMPLE 2
Example 1 was repeated, only the Tetrol having a molecular weight
of 405 was replaced with the following triol having a molecular
weight of 2,540:
A liquid triol (polyoxypropylene derivative of trimethylol propane)
having a molecular weight of 2,540, a functionality of 3, and an
hydroxyl number of 64.
Excellent properties of the coating were also obtained.
EXAMPLE 3
Example 1 was repeated, only the reactive solvent was omitted from
the reaction ingredients.
The resins of Examples 2 and 3 were evaluated in clear coatings on
steel. The following results were obtained when coating was applied
by a Bird applicator onto zinc phosphate treated steel panels to
deposit a wet coating having a thickness of 3 mils and the coated
steel panels were baked in an electric oven at 350.degree.F. for 20
minutes.
______________________________________ Properties Example 2 Example
3 ______________________________________ Hardness (pencil) 4H 4H
Impact (Forward 80 inch/lb.) Pass Fail Impact (Reverse 60 inch/lb.)
Pass Fail Flexibility (1/4 inch Mandrel) Pass Fail Solvent
Resistance (50 methyl ethyl ketone rubs) Pass Pass
______________________________________
EXAMPLE 4
Parts by Weight
1.
240 Neopentyl Glycol
1070 2,2-Dimethyl-3-hydroxypropyl-2,2-Dimethyl-3-Hydroxypropionate
(see the structure of Ester Diol 204 presented hereinbefore)
175 Isophthalic Acid
650 Trimellitic Anhydride
2 Dibutyl Tin Oxide (catalyst)
50 Xylol (reflux solvent)
Set trap with xylol. Heat to 210.degree.C. and collect water in
trap. When 110 grams of water are collected, cool to 190.degree.C.
and hold for a final acid value of 50-53. Total water collected,
135 grams. Remove trap and blow off xylol using nitrogen
sparge.
2. 909 Tetrol (molecular weight 594 - see Note 2)
3. 727 Hexamethoxy Methyl Melamine
4. 727 2-Ethoxy Ethanol
5. 160 Dimethyl Ethanol Amine
6. 2909 Deionized Water
Add reactive solvent 2 and cool to 80.degree.C. Add water soluble
melamine 3, solvent 4, amine 5, and water 6.
______________________________________ Final Characteristics
______________________________________ Solids (percent) 48.9
Gardner viscosity Z.sub.1 - Z.sub.2 Color (Gardner-Holdt) 1-2
______________________________________ Note 2 Polyoxypropylene
derivative of pentaerythritol, molecular weight: 594;
functionality: 4; hydroxyl number: 378; and viscosity: 1200
centipoises a 25.degree.C.
______________________________________ Ratio of Resin Solids: Water
Soluble Polyester: 55% Reactive Polyol Solvent 25%
Hexamethoxymethyl Melamine (Cross- linking agent) 20% Ratio of
Volatile Solvents: Deionized Water 80% 2-Ethoxy Ethanol 20%
______________________________________
Evaluation of Example 4 Resin
A white pigmented coating was prepared by dispersing titanium
dioxide pigment in the Example 4 resin solution utilizing high
speed mixing.
The final characteristics of the white coatings were:
Pigment (titanium dioxide) ratio to resin solids: 1:1
Viscosity (No. 4 Ford Cup) 61 seconds
Total solids: 59.5%
The following results were obtained, when the coating was applied
by a Bird applicator onto zinc phosphate treated steel panels to
deposit a wet coating having a thickness of about 3 mils and the
coated panels were baked at 300.degree.F. for 20 minutes in an
electric oven.
______________________________________ Properties Example 4
______________________________________ Gloss (photovolt 60.degree.)
93 Pencil hardness 6H Impact (forward 80 inch/lb.) Pass Impact
(reverse 40 inch/lb.) Pass Flexibility (1/4 inch Mandrel) Pass
Solvent Resistance (50 methyl ethyl Pass ketone rubs) Stain
resistance to mustard, lipstick, and cottonseed oil Excellent
______________________________________
EXAMPLE 5
Example 4 is repeated except that the Tetrol defined in Note 2 is
replaced on an equi-weight basis by the following caprolactone
triol:
Functionality: 3
Melting Point, .degree.C.: 27-32
Hydroxyl Number: 187
Viscosity at 40.degree.C.: 560 centistokes
Specific Gravity at 40.degree.C.: 1.084
Approximately the same results reported in Example 4 are obtained
except that the hardness was not quite as great, and the coatings
possess superior resistance to yellowing, particularly on
overbake.
In place of the caprolactone triol notes above, a commercially
available product NIAX Carpolactone Polyol PCP-0310 (Trademark) may
be used. This product is available from Union Carbide Chemicals
Company, New York, N.Y.
The invention is defined in the claims which follow.
* * * * *